JP6603329B2 - Thermoplastic resin composition and molded article thereof - Google Patents

Description

  The present invention relates to a thermoplastic resin composition having excellent impact resistance at low temperatures and suppressing delamination of stretch blow molded containers.

In recent years, there has been a movement to replace fire extinguishers and LPG containers, which have conventionally used only metals, with resin due to deregulation in Japan. Compared to metal containers, resin containers have advantages such as being light and easy to carry, resistant to corrosion, and excellent design.
In oxygen, nitrogen, and CNG cylinders that require high pressure resistance as containers, when releasing and using the internal gas, the internal pressure is suddenly released, resulting in a decrease in temperature. Is required. In addition, when storing gas in a container in a liquid state, physical properties that are difficult to become brittle in a lower temperature range are required. For this reason, physical property modification of a thermoplastic resin that is easily embrittled in a low-temperature region as compared with metal is indispensable for use in a pressure-resistant container or a liquid gas storage container. Aromatic polyesters typified by polyethylene terephthalate and polyethylene naphthalate have high strength, transparency, chemical resistance, heat resistance and gas barrier properties when drawn, and are used in various containers. However, since embrittlement occurs in the low temperature region, it has been difficult to apply to the above-described pressure vessel and liquid gas storage vessel.

  Japanese Patent Laid-Open No. 63-238155 exemplifies a composition composed of polyethylene naphthalate and a polyester elastomer. However, the glass transition temperature of the polyester elastomer is about −40 ° C., and there is a problem that sufficient impact resistance cannot be obtained in a temperature range below that. JP-T-2008-545018 discloses a composition containing an ethylene / α-olefin copolymer in a thermoplastic resin. The ethylene / α-olefin copolymer has a glass transition temperature of −60 ° C. or lower, and has an advantage of excellent impact resistance in a low temperature region. However, the ethylene / α-olefin copolymer is poorly compatible with a thermoplastic resin having a carboxyl group at a part of the terminal represented by polyester, and the ethylene / α-olefin copolymer and its thermoplastic resin However, this composition has a problem that sufficient impact resistance cannot be obtained and delamination occurs when stretch blow molding is performed. Japanese Patent Application Laid-Open No. 2011-256276 describes that an ethylene / propylene / butadiene copolymer component and an ethylene glycidyl methacrylate copolymer component may be used in combination with a resin component containing an aromatic polyester. The ethylene glycidyl methacrylate copolymer has the characteristic of acting as a compatibilizer, and thus effectively acts on delamination during stretch blow molding, but has a methacrylate unit, which is a hard component, and thus has low-temperature resistance. There was a problem of deteriorating impact properties.

JP 63-238155 A Special table 2008-545018 gazette JP 2011-256276 A

  The objective of this invention is providing the thermoplastic resin composition which is excellent in the impact resistance in low temperature, and suppresses the delamination of a stretch blow molding container.

Still other objects and advantages of the present invention will become apparent from the following description.
As a result of intensive research aimed at achieving the above object, the present inventors have found that an aromatic polyester resin has an ethylene / α-olefin copolymer, an epoxy group-containing silicon elastomer having a low glass transition temperature, and an antioxidant. By adding, it discovered that the resin composition which was excellent in low temperature impact resistance and suppressed the delamination of a stretch blow molding container was obtained, and came to solve the said subject.
That is, according to the present invention, the above objects and advantages of the present invention are as follows: (A) 5 to 80 parts by weight of an ethylene / α-olefin copolymer and (C) an epoxy with respect to 100 parts by weight of an aromatic polyester resin. Resin containing 1 to 30 parts by weight of a group-containing silicon elastomer and (D) 0.01 to 3 parts by weight of at least one antioxidant selected from the group consisting of hindered phenol compounds, phosphite compounds, phosphonite compounds and thioether compounds Achieved by the composition.

  The resin composition of the present invention is excellent in low-temperature impact resistance and suppresses delamination when formed into a container by stretch blow molding, so various pressure vessels such as LPG cylinders, carbon dioxide cylinders, oxygen cylinders, natural gas cylinders, etc. It is very useful in industry.

It is a side view of the preform created in Example 1 of the present invention. It is a side view of the blow molded object created in Example 1 of this invention.

Hereinafter, the preparation method and molding processing method of the resin used in the present invention will be sequentially described.
<About resin components>
The resin composition of the present invention, including the aromatic polyester resin (A component). In concrete terms, polyethylene terephthalate, polybutylene terephthalate, polyethylene naphthalate, polybutylene naphthalate, aromatic polyester Le such as polypropylene terephthalate are exemplified. Chemical resistance, heat resistance, strength, because a good balance of gas barrier properties, aromatic polyester is preferable.

  As the aromatic polyester, the dicarboxylic acid component and diol component forming the polyester are preferably 70 mol% or more, more preferably 90 mol% or more, and most preferably 99 mol% or more of the total dicarboxylic acid component. An aromatic polyester resin that is an acid component is preferred.

  Examples of the dicarboxylic acid include terephthalic acid, isophthalic acid, 2-chloroterephthalic acid, 2,5-dichloroterephthalic acid, 2-methylterephthalic acid, 4,4′-stilbene dicarboxylic acid, and 4,4′-biphenyl. Dicarboxylic acid, orthophthalic acid, 2,6-naphthalenedicarboxylic acid, 2,7-naphthalenedicarboxylic acid, bisbenzoic acid, bis (p-carboxyphenyl) methane, anthracene dicarboxylic acid, 4,4′-diphenyl ether dicarboxylic acid, 4, Examples thereof include 4'-diphenoxyethanedicarboxylic acid, 5-Na sulfoisophthalic acid, ethylene-bis-p-benzoic acid and the like. These dicarboxylic acids can be used alone or in admixture of two or more. In addition to the above aromatic dicarboxylic acid component, the aromatic polyester can be copolymerized with an aliphatic dicarboxylic acid component of less than 30 mol%. Specific examples of the aromatic dicarboxylic acid include adipic acid, sebacic acid, azelaic acid, dodecanedioic acid, 1,3-cyclohexanedicarboxylic acid, 1,4-cyclohexanedicarboxylic acid and the like.

  Examples of the diol of the diol component of the aromatic polyester include ethylene glycol, diethylene glycol, 1,2-propylene glycol, 1,3-propanediol, 2,2-dimethyl-1,3-propanediol, trans- or cis-2. , 2,4,4-tetramethyl-1,3-cyclobutanediol, 1,4-butanediol, neopentyl glycol, 1,5-pentanediol, 1,6-hexanediol, 1,4-cyclohexanedimethanol, Examples include 1,3-cyclohexanedimethanol, decamethylene glycol, cyclohexanediol, p-xylenediol, bisphenol A, tetrabromobisphenol A, and tetrabromobisphenol A-bis (2-hydroxyethyl ether). These can be used alone or in combination of two or more. The amount of the dihydric phenol component used in the diol component is preferably 30 mol% or less.

  Among the aromatic polyesters, polyethylene terephthalate and polyethylene naphthalate having excellent stretch blow moldability are more preferable, and polyethylene naphthalate having excellent chemical resistance, heat resistance, strength, and gas barrier properties are particularly preferable.

As the polyethylene naphthalate, the dicarboxylic acid component is composed of 80 to 100 mol% of naphthalenedicarboxylic acid component and 0 to 20 mol% of one selected from the group consisting of a terephthalic acid component and an isophthalic acid component, and the diol component is an ethylene glycol component Polyethylene naphthalate consisting of Further preferable copolymerization ratios of the dicarboxylic acid component are 85 to 100 mol% of the naphthalenedicarboxylic acid component and 0 to 15 mol% of the terephthalic acid component and the isophthalic acid component. When the copolymerization ratio of the terephthalic acid component and / or isophthalic acid component of the dicarboxylic acid component exceeds 20 mol%, the crystallinity is lowered, the thickness of the body portion is reduced at the time of blow molding, and the gas barrier property is rapidly deteriorated. Become.
The intrinsic viscosity (IV) of polyethylene naphthalate is preferably 0.5 to 1.0 dl / g, more preferably 0.55 to 0.90 dl / g, still more preferably 0.6 to 0.85 dl / g. g. If the intrinsic viscosity is greater than 1.0 dl / g, the appearance of the gate portion (bottom of the container) may be whitened due to an increase in resin pressure applied during injection molding. When the intrinsic viscosity is less than 0.5 dl / g, the crystallinity of polyethylene naphthalate increases, and it may crystallize when a thick preform is molded and may be damaged during blow molding. Intrinsic viscosity is as follows: 0.6 g of resin is heated and melted in 50 ml of a mixed solvent of phenol / tetrachloroethane = 3/2 (weight ratio) and then cooled to room temperature. The viscosity of the resulting resin solution is measured using an Ostwald type viscosity tube. It was measured under the temperature condition of 35 ° C. and obtained from the obtained solution viscosity data.

  Regarding the method for producing the aromatic polyester resin, the dicarboxylic acid or dicarboxylic acid ester and the diol component are polymerized while heating in the presence of a polycondensation catalyst containing titanium, germanium, antimony, etc. according to a conventional method. This is done by discharging the raw water or lower alcohol out of the system. For example, germanium-based polymerization catalysts include germanium oxides, hydroxides, halides, alcoholates, phenolates, and the like. More specifically, germanium oxide, germanium hydroxide, germanium tetrachloride, tetramethoxygermanium, and the like can be given. Further, in the present invention, compounds such as manganese, zinc, calcium, magnesium, etc., which are used in a transesterification reaction that is a prior stage of a conventionally known polycondensation, can be used in combination, and phosphoric acid or phosphorous after completion of the transesterification reaction. Such a catalyst can be deactivated and polycondensed with an acid compound or the like. Furthermore, the production method of the aromatic polyester resin can be either batch type or continuous polymerization type, but the continuous polymerization type is preferable. This is because the quality stability is high and the cost is advantageous.

<About ethylene / α-olefin copolymer>
In the present invention, an ethylene / α-olefin copolymer (component B) is included as a soft component. The ethylene / α-olefin copolymer is a copolymer obtained by copolymerizing ethylene and an α-olefin having 3 or more carbon atoms. The α-olefin having 3 or more carbon atoms is preferably an α-olefin having 3 to 20 carbon atoms, such as propylene, 1-butene, 1-pentene, 1-hexene, 1-heptene, 1-octene, 1-nonene, 1-decene, 1-undecene, 1-dodecene, 1-tridecene, 1-tetradecene, 1-pentadecene, 1-hexadecene, 1-heptadecene, 1-octadecene, 1-nonadecene, 1-eicosene, 3-methyl-1- Butene, 3-methyl-1-pentene, 3-ethyl-1-pentene, 4-methyl-1-pentene, 4-methyl-1-hexene, 4,4-dimethyl-1-hexene, 4,4-dimethyl- 1-pentene, 4-ethyl-1-hexene, 3-ethyl-1-hexene, 9-methyl-1-decene, 11-methyl-1-dodecene, 12-ethyl- 1-tetradecene etc. are mentioned. These can use 1 type (s) or 2 or more types. In addition, a non-conjugated diene can be further copolymerized with the copolymer. Non-conjugated dienes include, for example, 1,4-pentadiene, 1,4-hexadiene, 1,5-hexadiene, 1,4-octadiene, 1,5-octadiene, 1,6-octadiene, 1,7-octadiene, 2 -Methyl-1,5-hexadiene, 6-methyl-1,5-heptadiene, 7-methyl-1,6-octadiene, 4-ethylidene-8-methyl-1,7-nonadiene, 4,8-dimethyl-1 , 4,8-decatriene (DMDT), dicyclopentadiene, cyclohexadiene, cyclooctadiene, 5-vinylnorbornene, 5-ethylidene-2-norbornene, 5-methylene-2-norbornene, 5-isopropylidene-2-norbornene 6-chloromethyl-5-isopropenyl-2-norbornene, 2,3-diisopropylidene-5 Norbornene, 2-ethylidene-3-isopropylidene-5-norbornene, and 2-propenyl-2,5-norbornadiene. These can use 1 type (s) or 2 or more types.

The non-conjugated diene is preferably copolymerized in a proportion of 14% by weight or less based on the total weight of ethylene and α-olefin.
In the present invention, the ethylene / α-olefin copolymer is preferably modified with an unsaturated carboxylic acid. By modifying with unsaturated carboxylic acid or its acid derivative, affinity with resin as component A is improved, impact resistance at low temperature is improved, and delamination of containers obtained by stretch blow molding Is suppressed. Examples of the unsaturated carboxylic acid include unsaturated carboxylic acids such as maleic acid, fumaric acid, tetrahydrophthalic acid, itaconic acid, citraconic acid, crotonic acid, isocrotonic acid, nadic acid, acrylic acid and methacrylic acid. Examples of the acid derivative include acid anhydrides, imides, amides and esters of the above unsaturated carboxylic acids. Specific examples of the derivative include maleimide, maleic anhydride, citraconic anhydride, monomethyl maleate, glycidyl malate, and the like. Among these, unsaturated carboxylic acids or acid anhydrides thereof are preferable, and maleic acid, nadic acid, and acid anhydrides thereof are particularly preferable. The modification amount of the unsaturated carboxylic acid is preferably from 0.5 to 4 mol%, more preferably from 1 to 3 mol%, based on 100 mol% of the ethylene / α-olefin copolymer. If the modification amount of the unsaturated carboxylic acid is less than 0.5 mol%, the effect of improving the compatibility with the resin as the component A may not be sufficiently obtained. If it exceeds 4 mol%, an epoxy group-containing silicon elastomer ( C component) may cause excessive reaction and may cause poor appearance due to gelation.

  In order to efficiently react the unsaturated carboxylic acid or its acid derivative with an ethylene / α-olefin copolymer to obtain a modified product, the reaction is preferably carried out in the presence of a radical initiator. The reaction is usually carried out at a temperature of 60 to 350 ° C. The ratio of the radical initiator used is preferably in the range of 0.001 to 2 parts by weight with respect to 100 parts by weight of the ethylene / α-olefin copolymer. Examples of the radical initiator include dicumyl peroxide, di-tert-butyl peroxide, 2,5-dimethyl-2,5-di (tert-butylperoxy) hexyne-3, 2,5-dimethyl-2, Organic peroxides such as 5-di (tert-butylperoxy) hexane and 1,4-bis (tert-butylperoxyisopropyl) benzene are preferred.

  Content of B component of this invention is 5-80 weight part with respect to 100 weight part of A component, Preferably it is 7-65 weight part, More preferably, it is 10-60 weight part. When the content of the B component is less than 5 parts by weight, the effect of improving the low temperature impact resistance cannot be sufficiently obtained.

<About epoxy group-containing silicon elastomer>
The resin composition of the present invention contains an epoxy group-containing silicon elastomer (component C).
The silicone elastomer having a low glass transition temperature contains an epoxy group, so that the compatibility between the A component and the B component can be improved, and the low temperature impact resistance of the resulting resin composition is improved and stretch blow molding. Container delamination is suppressed.

Examples of the C component silicon elastomer include silicon elastomers obtained by three-dimensionally cross-linking linear organopolysiloxanes (JP-A 63-77942, JP-A-3-93934, JP-A 04-198324). And a silicon elastomer obtained by pulverization (see U.S. Pat. No. 3,843,601, JP-A-62-270660, JP-A-59-96122), and silicon obtained by the above method Polyorganosilsesquioxane having a structure in which the surface of the elastomer is crosslinked in a three-dimensional network represented by (R′SiO _3/2 ) n (R ′ represents a substituted or unsubstituted monovalent hydrocarbon group) Examples include silicon composite elastomers (see Japanese Patent Laid-Open No. 7-196815) with a structure coated with a cured silicone resin. You can. Component C is obtained by modifying these elastomers with an epoxy group.

The average particle size of the component C of the present invention is preferably from 0.01 to 50 μm, more preferably from 0.05 to 30 μm. When the average particle size is less than 0.01 μm, sufficient low-temperature impact resistance may not be obtained. When the average particle size is more than 50 μm, fine stretch may appear on the container surface and damage the appearance when stretch blow molding is performed. . The average particle diameter can be measured by a laser light diffraction scattering method.
Examples of such an epoxy group-containing silicon elastomer include those commercially available from Toray Dow Corning Silicone Co., Ltd. under the trade name of Trefil EP-2601.

  Content of C component of this invention is 1-30 weight part with respect to 100 weight part of A component, Preferably it is 3-20 weight part, More preferably, it is 5-15 weight part. When the content of component C is less than 1 part by weight, it does not function sufficiently as a compatibilizing agent, improves the impact resistance at room temperature (23 ° C.) and at low temperatures, and suppresses delamination of containers obtained by stretch blow molding. When the effect is not sufficiently obtained and the amount is more than 30 parts by weight, the appearance defect due to the rough surface occurs in the container obtained by stretch blow molding.

<About acid value inhibitor>
In the present invention, at least one antioxidant selected from the group consisting of hindered phenol compounds, phosphite compounds, phosphonite compounds and thioether compounds is used as the antioxidant (component D). By blending such an antioxidant in the composition, the reason for this is not clear, but surprisingly the low temperature impact resistance is improved.

  As the hindered phenol compound, for example, α-tocopherol, butylhydroxytoluene, sinapyl alcohol, vitamin E, n-octadecyl-β- (4′-hydroxy-3 ′, 5′-di-tert-butylphenol) propionate, 2-tert-butyl-6- (3′-tert-butyl-5′-methyl-2′-hydroxybenzyl) -4-methylphenyl acrylate, 2,6-di-tert-butyl-4- (N, N -Dimethylaminomethyl) phenol, 3,5-di-tert-butyl-4-hydroxybenzylphosphonate diethyl ester, 2,2'-methylenebis (4-methyl-6-tert-butylphenol), 2,2'-methylenebis ( 4-ethyl-6-tert-butylphenol), 4,4'-methylene Bis (2,6-di-tert-butylphenol), 2,2′-methylenebis (4-methyl-6-cyclohexylphenol), 2,2′-dimethylene-bis (6-α-methyl-benzyl-p-cresol) ), 2,2′-ethylidene-bis (4,6-di-tert-butylphenol), 2,2′-butylidene-bis (4-methyl-6-tert-butylphenol), 4,4′-butylidenebis (3 -Methyl-6-tert-butylphenol), triethylene glycol-N-bis-3- (3-tert-butyl-4-hydroxy-5-methylphenyl) propionate, 1,6-hexanediol bis [3- ( 3,5-di-tert-butyl-4-hydroxyphenyl) propionate], bis [2-tert-butyl-4-methyl- -(3-tert-butyl-5-methyl-2-hydroxybenzyl) phenyl] terephthalate, 3,9-bis {2- [3- (3-tert-butyl-4-hydroxy-5-methylphenyl) propionyloxy ] -1,1-dimethylethyl} -2,4,8,10-tetraoxaspiro [5,5] undecane, 4,4′-thiobis (6-tert-butyl-m-cresol), 4,4 ′ -Thiobis (3-methyl-6-tert-butylphenol), 2,2'-thiobis (4-methyl-6-tert-butylphenol), bis (3,5-di-tert-butyl-4-hydroxybenzyl) sulfide 4,4′-di-thiobis (2,6-di-tert-butylphenol), 4,4′-tri-thiobis (2,6-di-tert-butylphenol) Nol), 2,2-thiodiethylenebis- [3- (3,5-di-tert-butyl-4-hydroxyphenyl) propionate], 2,4-bis (n-octylthio) -6- (4-hydroxy -3 ′, 5′-di-tert-butylanilino) -1,3,5-triazine, N, N′-hexamethylenebis- (3,5-di-tert-butyl-4-hydroxyhydrocinnamide), N, N′-bis [3- (3,5-di-tert-butyl-4-hydroxyphenyl) propionyl] hydrazine, 1,1,3-tris (2-methyl-4-hydroxy-5-tert-butyl Phenyl) butane, 1,3,5-trimethyl-2,4,6-tris (3,5-di-tert-butyl-4-hydroxybenzyl) benzene, tris (3,5-di-tert-butyl) 4-hydroxyphenyl) isocyanurate, tris (3,5-di-tert-butyl-4-hydroxybenzyl) isocyanurate, 1,3,5-tris (4-tert-butyl-3-hydroxy-2, 6-dimethylbenzyl) isocyanurate, 1,3,5-tris {2- [3- (3,5-di-tert-butyl-4-hydroxyphenyl) propionyloxy] ethyl} isocyanurate, and tetrakis [methylene- 3- (3 ′, 5′-di-tert-butyl-4-hydroxyphenyl) propionate] methane and the like. Among the above compounds, tetrakis [methylene-3- (3-tert-butyl-4-hydroxy-5-methylphenyl) propionate] methane, octadecyl-3- (3,5-di-tert-butyl-4-hydroxyphenyl) ) Propionate and 3,9-bis [2- {3- (3-tert-butyl-4-hydroxy-5-methylphenyl) propionyloxy} -1,1-dimethylethyl] -2,4,8,10 -Tetraoxaspiro [5,5] undecane is preferred. Particularly preferred is octadecyl-3- (3,5-di-tert-butyl-4-hydroxyphenyl) propionate. All of these are readily available. The said hindered phenol compound can be used individually or in combination of 2 or more types.

  Examples of the phosphite compound include triphenyl phosphite, tris (nonylphenyl) phosphite, tridecyl phosphite, trioctyl phosphite, trioctadecyl phosphite, didecyl monophenyl phosphite, dioctyl monophenyl phosphite, diisopropyl mono Phenyl phosphite, monobutyl diphenyl phosphite, monodecyl diphenyl phosphite, monooctyl diphenyl phosphite, tris (diethylphenyl) phosphite, tris (di-iso-propylphenyl) phosphite, tris (di-n-butylphenyl) ) Phosphite, tris (2,4-di-tert-butylphenyl) phosphite, tris (2,6-di-tert-butylphenyl) phosphite, distearyl pen Erythritol diphosphite, bis (2,4-di-tert-butylphenyl) pentaerythritol diphosphite, bis (2,6-di-tert-butyl-4-methylphenyl) pentaerythritol diphosphite, bis (2 , 6-Di-tert-butyl-4-ethylphenyl) pentaerythritol diphosphite, bis {2,4-bis (1-methyl-1-phenylethyl) phenyl} pentaerythritol diphosphite, phenylbisphenol A pentaerythritol Examples thereof include diphosphite, bis (nonylphenyl) pentaerythritol diphosphite, and dicyclohexyl pentaerythritol diphosphite. Other phosphite compounds having a cyclic structure by reacting with dihydric phenols, such as 2,2′-methylenebis (4,6-di-tert-butylphenyl) (2,4-di-tert-butylphenyl) Phosphites, 2,2′-methylenebis (4,6-di-tert-butylphenyl) (2-tert-butyl-4-methylphenyl) phosphite, and 2,2-methylenebis (4,6-di-tert) -Butylphenyl) octyl phosphite can also be used. Among these, suitable phosphite compounds are distearyl pentaerythritol diphosphite, bis (2,4-di-tert-butylphenyl) pentaerythritol diphosphite, bis (2,6-di-tert-butyl- 4-methylphenyl) pentaerythritol diphosphite and bis {2,4-bis (1-methyl-1-phenylethyl) phenyl} pentaerythritol diphosphite.

  Furthermore, as a diphosphite compound, for example, 2,4,8,10-tetra-t-butyl-6- [3- (3-methyl-4-hydroxy-5-t-butylphenyl) propoxy] dibenzo [d, f] [1,3,2] dioxaphosphepine [commercially available product of “Sumilyzer GP” (manufactured by Sumitomo Chemical Co., Ltd.)], 2,10-dimethyl-4,8-di-t-butyl-6- [3- (3,5-di-t-butyl-4-hydroxyphenyl) propoxy] -12H-dibenzo [d, g] [1,3,2] dioxaphosphocine, 2,4,8,10-tetra-t -Butyl-6- [3- (3,5-di-t-butyl-4-hydroxyphenyl) propoxy] dibenzo [d, f] [1,3,2] dioxaphosphine, 2,4,8 , 10-Tetra-t-pentyl-6- [3- (3,5- -T-butyl-4-hydroxyphenyl) propoxy] -12-methyl-12H-dibenzo [d, g] [1,3,2] dioxaphosphocin, 2,10-dimethyl-4,8-di-t -Butyl-6- [3- (3,5-di-t-butyl-4-hydroxyphenyl) propionyloxy] -12H-dibenzo [d, g] [1,3,2] dioxaphosphocine, 2, 4,8,10-Tetra-t-pentyl-6- [3- (3,5-di-t-butyl-4-hydroxyphenyl) propionyloxy] -12-methyl-12H-dibenzo [d, g] [ 1,3,2] dioxaphosphocin, 2,4,8,10-tetra-t-butyl-6- [3- (3,5-di-t-butyl-4-hydroxyphenyl) propionyloxy]- Dibenzo [d, f] [1,3,2] dio Saphosfepine, 2,10-dimethyl-4,8-di-t-butyl-6- (3,5-di-t-butyl-4-hydroxybenzoyloxy) -12H-dibenzo [d, g] [1,3 , 2] dioxaphosphocin, 2,4,8,10-tetra-t-butyl-6- (3,5-di-t-butyl-4-hydroxybenzoyloxy) -12-methyl-12H-dibenzo [ d, g] [1,3,2] dioxaphosphocin, 2,10-dimethyl-4,8-di-t-butyl-6- [3- (3-methyl-4-hydroxy-5-t- Butylphenyl) propoxy] -12H-dibenzo [d, g] [1,3,2] dioxaphosphocin, 2,4,8,10-tetra-t-butyl-6- [3- (3,5- Di-t-butyl-4-hydroxyphenyl) propoxy] -12H-dibe Nzo [d, g] [1,3,2] dioxaphosphocin, 2,10-diethyl-4,8-di-t-butyl-6- [3- (3,5-di-t-butyl) -4-hydroxyphenyl) propoxy] -12H-dibenzo [d, g] [1,3,2] dioxaphosphocin, 2,4,8,10-tetra-t-butyl-6- [2,2- Dimethyl-3- (3-tert-butyl-4-hydroxy-5-methylphenyl) propoxy] -dibenzo [d, f] [1,3,2] dioxaphosphine can be used. All of these are readily available. The said phosphite compound can be used individually or in combination of 2 or more types.

  Examples of the phosphonite compound include tetrakis (2,4-di-tert-butylphenyl) -4,4′-biphenylenediphosphonite, tetrakis (2,4-di-tert-butylphenyl) -4,3′-biphenyl. Range phosphonite, tetrakis (2,4-di-tert-butylphenyl) -3,3'-biphenylene diphosphonite, tetrakis (2,6-di-tert-butylphenyl) -4,4'-biphenylene diphospho Knight, tetrakis (2,6-di-tert-butylphenyl) -4,3′-biphenylene diphosphonite, tetrakis (2,6-di-tert-butylphenyl) -3,3′-biphenylene diphosphonite, Bis (2,4-di-tert-butylphenyl) -4-phenyl-phenylphosphonite, bis (2, -Di-tert-butylphenyl) -3-phenyl-phenylphosphonite, bis (2,6-di-n-butylphenyl) -3-phenyl-phenylphosphonite, bis (2,6-di-tert-butyl) Phenyl) -4-phenyl-phenylphosphonite, bis (2,6-di-tert-butylphenyl) -3-phenyl-phenylphosphonite, and the like. Of these, tetrakis (di-tert-butylphenyl) -biphenylenediphosphonites and bis (di-tert-butylphenyl) -phenyl-phenylphosphonites are preferred, and tetrakis (2,4-di-tert-butyl). More preferred are phenyl) -biphenylene diphosphonite and bis (2,4-di-tert-butylphenyl) -phenyl-phenylphosphonite. Such a phosphonite compound is preferable because it can be used in combination with a phosphite compound having an aryl group in which two or more alkyl groups are substituted. As the phosphonite compound, tetrakis (2,4-di-tert-butylphenyl) -biphenylene diphosphonite is preferable. This phosphonite-based antioxidant is commercially available as Sandostab P-EPQ (trademark, manufactured by Clariant) and Irgafos P-EPQ (trademark, manufactured by CIBA SPECIALTY CHEMICALS). The said phosphonite compound can be used individually or in combination of 2 or more types.

  Examples of the thioether compound include dilauryl thiodipropionate, ditridecyl thiodipropionate, dimyristyl thiodipropionate, distearyl thiodipropionate, pentaerythritol-tetrakis (3-lauryl thiopropionate), pentaerythritol. -Tetrakis (3-dodecylthiopropionate), pentaerythritol-tetrakis (3-octadecylthiopropionate), pentaerythritol tetrakis (3-myristylthiopropionate), pentaerythritol-tetrakis (3-stearylthiopropionate) Nate) and the like. The said thioether compound can be used individually or in combination of 2 or more types.

  Moreover, it is preferable to use in combination with 2 or more types in the said hindered phenol compound, a phosphite compound, a phosphonite compound, and a thioether compound as antioxidant. By using two or more of hindered phenol compounds, phosphite compounds, phosphonite compounds, and thioether compounds in combination, a synergistic effect is exhibited as an antioxidant, which is more effective in improving low-temperature impact resistance. .

  Content of D component is 0.01-3 weight part with respect to 100 weight part of A component, Preferably it is 0.03-2 weight part, More preferably, it is 0.05-1 weight part. When the content of the D component is less than 0.01 parts by weight, the antioxidant effect is insufficient and the low temperature impact resistance is also deteriorated. Further, when the content is more than 3 parts by weight, the hue is deteriorated by a reaction component derived from an antioxidant and the like.

<Other ingredients>
<Release agent>
The resin composition of the present invention can contain a release agent. Specific examples of release agents include fatty acids, fatty acid metal salts, oxy fatty acids, paraffins, low molecular weight polyolefins, fatty acid amides, alkylene bis fatty acid amides, aliphatic ketones, fatty acid partial saponified esters, fatty acid lower alcohol esters, fatty acid polyvalents. Examples thereof include alcohol esters, fatty acid polyglycol esters, and modified silicones. By blending these, a molded product excellent in mechanical properties, moldability, and heat resistance can be obtained.

  Fatty acids having 6 to 40 carbon atoms are preferred. Specifically, oleic acid, stearic acid, lauric acid, hydroxystearic acid, behenic acid, arachidonic acid, linoleic acid, linolenic acid, ricinoleic acid, palmitic acid, montan Examples thereof include acids and mixtures thereof. The fatty acid metal salt is preferably an alkali (earth) metal salt of a fatty acid having 6 to 40 carbon atoms, and specific examples include calcium stearate, sodium montanate, and calcium montanate.

Examples of the oxy fatty acid include 1,2-oxystearic acid. Paraffin having 18 or more carbon atoms is preferable, and examples thereof include liquid paraffin, natural paraffin, microcrystalline wax, petrolactam and the like.
The low molecular weight polyolefin preferably has a molecular weight of 5000 or less, and specifically includes polyethylene wax, maleic acid-modified polyethylene wax, oxidized type polyethylene wax, chlorinated polyethylene wax, polypropylene wax and the like.

As the fatty acid amide, those having 6 or more carbon atoms are preferable, and specific examples include oleic acid amide, erucic acid amide, and behenic acid amide.
The alkylene bis fatty acid amide is preferably one having 6 or more carbon atoms, and specifically includes methylene bis stearic acid amide, ethylene bis stearic acid amide, N, N-bis (2-hydroxyethyl) stearic acid amide and the like.
As the aliphatic ketone, those having 6 or more carbon atoms are preferable, and examples thereof include higher aliphatic ketones.

Examples of the fatty acid partially saponified ester include montanic acid partially saponified ester. Examples of the fatty acid lower alcohol ester include stearic acid ester, oleic acid ester, linoleic acid ester, linolenic acid ester, adipic acid ester, behenic acid ester, arachidonic acid ester, montanic acid ester, isostearic acid ester and the like.
Examples of fatty acid polyhydric alcohol esters include glycerol tristearate, glycerol distearate, glycerol monostearate, pentaerythritol tetrastearate, pentaerythritol tristearate, pentaerythritol dimyristate, pentaerythr Examples include rutol monostearate, pentaerythritol adipate stearate, and sorbitan monobehenate.

Examples of fatty acid polyglycol esters include polyethylene glycol fatty acid esters, polytrimethylene glycol fatty acid esters, and polypropylene glycol fatty acid esters.
Examples of the modified silicone include polyether-modified silicone, higher fatty acid alkoxy-modified silicone, higher fatty acid-containing silicone, higher fatty acid ester-modified silicone, methacryl-modified silicone, and fluorine-modified silicone.

  Of these, fatty acid, fatty acid metal salt, oxy fatty acid, fatty acid ester, fatty acid partial saponified ester, paraffin, low molecular weight polyolefin, fatty acid amide, and alkylene bis fatty acid amide are preferred, and fatty acid partial saponified ester and alkylene bis fatty acid amide are more preferred. In particular, montanic acid ester, montanic acid partial saponified ester, polyethylene wax, acid value polyethylene wax, sorbitan fatty acid ester, erucic acid amide, ethylene bis stearic acid amide are preferable, and in particular, montanic acid partial saponified ester and ethylene bis stearic acid amide are preferable. Particularly preferred. A mold release agent may be used by 1 type and may be used in combination of 2 or more type. The content of the release agent is preferably 0.01 to 3 parts by weight, more preferably 0.03 to 2 parts by weight, with respect to 100 parts by weight of component A.

<Heating aid>
The resin composition of the present invention can contain a heating aid for the purpose of improving the heating efficiency of the infrared (IR) heater during blow molding and shortening the heating time. Such heating aids include, for example, phthalocyanine near-infrared absorbers, metal oxides near-infrared absorbers such as ATO, ITO, iridium oxide and ruthenium oxide and imonium oxide, metals such as lanthanum boride, cerium boride and tungsten boride. Various metal compounds having excellent near-infrared absorption ability, such as borides and tungsten oxide near-infrared absorbers, are preferred. As such a phthalocyanine near infrared absorber, for example, MIR-362 manufactured by Mitsui Chemicals, Inc. is easily available as a commercial product. These may be used alone or in combination of two or more. The content of the phthalocyanine near-infrared absorber is preferably 0.0005 to 0.2 parts by weight, more preferably 0.0008 to 0.1 parts by weight, with respect to 100 parts by weight of the component A, and 0.001 to 0.07. Part by weight is more preferred. If the content is less than 0.0005 parts by weight, the effect as a heating aid may not be sufficiently obtained, and it may take a long time to heat the preform during blow molding. Moreover, when this content is more than 0.2 parts by weight, the heating aid may bleed out during blow molding overheating. The content of the metal oxide near-infrared absorber, metal boride near-infrared absorber, and tungsten oxide infrared absorber is preferably in the range of 0.1 to 500 ppm (by weight) in the resin, and in the range of 0.5 to 300 ppm. Is more preferable. If the content is less than 0.1 ppm, the effect as a heating aid may not be sufficiently obtained, and it may take a long time to heat the preform during blow molding. In addition, when the content is more than 500 ppm, the resin component may be greatly decomposed. When the carbon filler is contained, it is difficult to uniformly heat the preform to the inside. Therefore, it is recommended that the carbon filler is not included.

<Other resins>
The resin composition of the present invention may contain another resin different from the component A within a range not departing from the spirit of the present invention. Examples of such other resins include thermosetting resins such as phenol resins, melamine resins, silicone resins, and epoxy resins, polycarbonate resins, polyimide resins, polyetherimide resins, polyphenylene ether resins, polysulfone resins, polystyrene resins, acrylonitrile / styrene. Examples thereof include thermoplastic resins such as a copolymer (AS resin), a polystyrene resin, a high-impact polystyrene resin, and a syndiotactic polystyrene resin. The content of these other resins is preferably 1 to 80 parts by weight and more preferably 3 to 50 parts by weight with respect to 100 parts by weight of component A.

<Preparation of resin composition>
The resin composition of the present invention is produced by mixing the A component, B component, C component, D component and other additive components.
Other additive components include UV absorbers, light stabilizers, flow modifiers, colorants, light diffusing agents, fluorescent brighteners, phosphorescent pigments, fluorescent dyes, antistatic agents, antibacterial agents, crystal nucleating agents, plasticizers Arbitrary additive components, such as an agent, are mentioned.

  In order to produce the resin composition of the present invention, various methods are employed. For example, a method of premixing the component A and other components, then melt-kneading and pelletizing can be mentioned as one preferred method. Examples of the premixing means include a Nauter mixer, a V-type blender, a Henschel mixer, a mechanochemical apparatus, and an extrusion mixer. In the preliminary mixing, granulation can be performed by an extrusion granulator or a briquetting machine depending on the case. After the preliminary mixing, the mixture is melt-kneaded by a melt-kneader represented by a vent type twin-screw extruder and pelletized by a device such as a pelletizer. As the melt kneader, a Banbury mixer, a kneading roll, a constant-temperature stirring vessel, and the like can be used, but a vent type twin screw extruder is preferable. In addition, a method of supplying each component independently to a melt-kneader represented by a twin-screw extruder can be employed without premixing each component.

<Manufacture of molded products>
The resin composition of the present invention is usually obtained as pellets produced by the above method. Pellets are suitable for producing container products by rotational molding and blow molding using these as raw materials. Examples of the blow molding method include direct blow molding, extrusion direct blow molding, one-stage stretch blow molding, and two-stage stretch blow molding. Of these, two-stage stretch blow molding is preferred because a container product excellent in strength, chemical resistance, gas barrier properties, and heat resistance can be obtained.

  Various preforming methods such as injection molding, press molding, and extrusion molding can be selected as a preform molding method when stretch blow molding is performed in two stages. Of these, injection molding and press molding are preferred from the viewpoint of rapid cooling without crystallizing the preform. In the injection molding, not only a normal cold runner molding method but also a hot runner molding method is possible. In such injection molding, not only a normal molding method but also injection compression molding, injection press molding, foam molding (including by supercritical fluid injection), insert molding, in-mold coating molding, as appropriate, depending on the purpose. A molded product can be obtained using an injection molding method such as rapid heating / cooling die molding.

When stretch blow molding is performed in two stages, heating (preliminary heating) can be performed in advance before blow molding. Such preheating temperature (glass transition temperature -40 ℃ aromatic polyester resin as the component A) - (glass transition temperature of the aromatic polyester resin is a component A + 40 ° C.) are preferred, (A Ingredient glass transition temperature -30 ° C.) ~ (a ingredient glass transition temperature + 30 ° C.), and most preferably from (a ingredient glass transition temperature -20 ° C. in) - (glass transition temperature of component a + 20 ° C.). If the preheating temperature is ( the glass transition temperature of the A component is less than −40 ° C.), it takes time for the main heating time in the post-process, and if the preheating temperature exceeds ( the glass transition temperature of the A component + 40 ° C.), the A component is Crystallization may cause damage to the container during blow molding. The preheating method may be any method such as storage of a preform in a hot air dryer or heating with an infrared heater. When the preform is thick, the heating at the time of blow molding (main heating) is preferably performed from both the heating from the inside of the preform (internal heating) and the heating from the outside of the preform (external heating). As the heating method, an infrared heating method is preferable since heating efficiency is good.

Furthermore, the molded product molded from the resin composition of the present invention is heated in a temperature range of ( A component glass transition temperature −40 ° C.) to ( A component glass transition temperature + 40 ° C.) regardless of the molding method. It is preferable to do. By heat-treating the molded article, an effect of improving low temperature impact resistance can be obtained. Although the mechanism by which the low temperature impact resistance is improved by heat treatment of the molded product is not clear, the effect of the C component as a compatibilizing agent is promoted by promoting the reaction between the epoxy group of the C component and the carboxyl group of the A component. It is presumed that this will increase. The heating temperature of the molded article, (glass transition temperature -30 ° C. of component A) - (glass transition temperature of component A + 30 ° C.) are more preferable, (glass transition temperature -20 ° C. of component A) - (Component A the glass transition temperature + 20 ° C.) being most preferred. When the heat treatment temperature is ( the glass transition temperature of component A is less than −40 ° C.), the effect of improving the low temperature impact resistance may not be obtained, and when the heat treatment temperature exceeds ( the glass transition temperature of component A + 40 ° C.) The molded body may be deformed. As a method of heat-treating the molded product, for example, any method such as storage of a molded body in a hot air dryer or a vacuum heat dryer, heating with an infrared heater, or the like can be employed. Although the time of this heat processing changes with the magnitude | sizes and thickness of a molded article, it can be 30 minutes-5 hours, for example.

  The molded body made of the resin composition of the present invention can be further imparted with other functions by surface modification. Surface modification here means a new layer on the surface of resin molded products such as vapor deposition (physical vapor deposition, chemical vapor deposition, etc.), plating (electroplating, electroless plating, hot dipping, etc.), painting, coating, printing, etc. The surface modification method used for ordinary resin molded products can be applied.

  Hereinafter, the present invention will be described in detail by way of examples. However, the present invention is not limited to these.

1. Production of Polymer Polyethylene naphthalate was produced by the method shown in the following production example. Moreover, the value of the intrinsic viscosity in a manufacture example was calculated | required by the following method.
(1) Intrinsic Viscosity (IV) Measurement Method 0.6 g of resin was melted by heating in 50 ml of a mixed solvent of phenol / tetrachloroethane = 3/2 (weight ratio), then cooled to room temperature, and the viscosity of the resulting resin solution Was measured using an Ostwald viscosity tube at a temperature of 35 ° C., and the intrinsic viscosity (IV) of the resin was determined from the obtained solution viscosity data.
(2) Production of Resin Production Examples 1-3: Polyethylene naphthalate (PEN-2, PEN-3, PEN-4)
The total number of moles of 2,6-naphthalenedicarboxylic acid dimethyl ester, terephthalic acid dimethyl ester, ethylene glycol, and 2,6-naphthalenedicarboxylic acid dimethyl ester as the transesterification catalyst prepared in quantities to give the polymer composition described in Table 1. 30 mmol% of cobalt acetate tetrahydrate and 70 mmol% of manganese acetate tetrahydrate with respect to the total number of moles of 2,6-naphthalenedicarboxylic acid dimethyl ester were fed to the reactor, and the reaction was conducted at 240 ° C. under a nitrogen atmosphere. The transesterification reaction was carried out. Subsequently, after adding antimony trioxide at 80 mmol% based on the total number of moles of 2,6-naphthalenedicarboxylic acid dimethyl ester, orthophosphoric acid was added based on the total number of moles of 2,6-naphthalenedicarboxylic acid dimethyl ester. 60 mmol% was added and held at 260 ° C. for 30 minutes. Thereafter, the temperature was increased and the pressure was gradually reduced, and finally polycondensation was performed at 300 ° C. and 0.1 kPa or less. The progress of the polycondensation reaction was confirmed by the load on the stirring blade, and the reaction was terminated when the desired degree of polymerization was reached. Thereafter, the reaction product in the system was continuously extruded in a strand form from the discharge part, cooled and cut to obtain about 3 mm granular pellets. The composition and physical properties of the obtained pellets are shown in Table 1.

2. Production and Evaluation of Resin Composition Pellet Production and blow molding of resin composition pellets were performed by the methods shown in the following Examples and Comparative Examples. Moreover, each value in an Example was calculated | required with the following method.
(1) Blow molded body evaluation (i) Axial misalignment The bottom of the blow molded body was visually observed.
(Ii) Breaking The appearance of the blow-molded product was visually observed. The case where the container was not torn was marked with ◯, and the number of tears was marked with x.
(Iii) Body Thickness After the body of the blow molded body was cut out to a size of 70 mm × 70 mm, the thickness was measured at 10 points at random, and the average value was calculated. The thickness required to be 200-540 μm.
(Iv) Appearance pearl tone The appearance of the blow-molded product was visually observed. The case where the container did not show a pearl tone due to delamination was rated as ◯, and the case where the pearl tone due to delamination was seen as x.
(V) Rough surface appearance The appearance of the blow molded article was visually observed. The case where the surface roughness was not observed in the container was marked with ◯, and the surface roughness was marked with x.
(Vi) Hue The appearance of the blow molded article was visually observed, and the container having a transparent or light yellow hue was marked with ◯, and the one with strong yellowishness was marked with x.

(2) Physical property evaluation (i) Charpy impact strength with notch at 23 ° C. Pellets obtained by the method described in the following examples were dried at 100 ° C. for 5 hours with a hot air circulation dryer, and injection molding machine (Toshiba Machine) A test piece conforming to the ISO standard with a thickness of 4 mm was molded at a cylinder temperature of 290 ° C., a mold temperature of 80 ° C., and a molding cycle of 50 seconds using IS-150EN. The obtained test piece was allowed to stand for 24 hours in an environment of a temperature of 23 ° C. and a relative humidity of 50%, and then the Charpy impact strength with a notch was measured according to the ISO standard.
(Ii) −60 ° C. Notched Charpy Impact Strength Pellets obtained by the method described in the following examples were dried at 100 ° C. for 5 hours with a hot air circulation dryer, and injection molding machine (manufactured by Toshiba Machine Co., Ltd.) : IS-150EN), a test piece conforming to the ISO standard having a thickness of 4 mm was molded at a cylinder temperature of 290 ° C., a mold temperature of 80 ° C., and a molding cycle of 50 seconds. The obtained test piece was left in a thermostatic bath at −60 ° C. for 6 hours, and then the test piece was quickly taken out from the thermostatic bath, and the notched Charpy impact strength was measured according to ISO standards.
(Iii) Notched Charpy impact strength with 23 ° C (after heat treatment)
The pellets obtained by the method described in the following examples were dried at 100 ° C. for 5 hours with a hot air circulation dryer, and cylinder temperature was measured using an injection molding machine (Toshiba Machine Co., Ltd .: IS-150EN). A test piece conforming to the ISO standard having a thickness of 4 mm was molded at 290 ° C., a mold temperature of 80 ° C., and a molding cycle of 50 seconds. The obtained test piece was heat-treated at 100 ° C. for 12 hours in a hot air dryer, left for 24 hours in an environment of a temperature of 23 ° C. and a relative humidity of 50%, and then subjected to notched Charpy impact strength in accordance with ISO standards. Was measured.
(Iv) -60 ° C notched Charpy impact strength (after heat treatment)
The pellets obtained by the method described in the following examples were dried at 100 ° C. for 5 hours with a hot air circulation dryer, and cylinder temperature was measured using an injection molding machine (Toshiba Machine Co., Ltd .: IS-150EN). A test piece conforming to the ISO standard having a thickness of 4 mm was molded at 290 ° C., a mold temperature of 80 ° C. and a molding cycle of 50 seconds. The obtained test piece was heat-treated at 100 ° C. for 12 hours with a hot air dryer and left in a thermostatic bath at −60 ° C. for 6 hours. Then, the test piece was quickly taken out of the thermostatic bath and conformed to ISO standards. The notched Charpy impact strength was measured.
In addition, the raw material as described below was used as each component other than PEN-2, PEN-3, and PEN-4.

<A component>
PEN-1: Teonex TR-8065S manufactured by Teijin Ltd. [polyethylene naphthalate produced from 100 mol% naphthalenedicarboxylic acid and 100 mol% ethylene glycol, intrinsic viscosity 0.67 dl / g]
PET-1: TRN-8550FF manufactured by Teijin Limited [polyethylene terephthalate manufactured from 100 mol% terephthalic acid and 100 mol% ethylene glycol, intrinsic viscosity 0.77 dl / g]
<B component>
B-1: Tuffmer DF605 [ethylene / propylene / 5-ethylidene-2-norbornene copolymer] manufactured by Mitsui Chemicals, Inc.
B-2: Tuffmer MH5020 manufactured by Mitsui Chemicals Co., Ltd. [Moleic acid 1 mol% modified ethylene / propylene / 5-ethylidene-2-norbornene copolymer]
B-3: Tuffmer MH5040 manufactured by Mitsui Chemicals Co., Ltd. [Moleic acid 2 mol% modified ethylene / propylene / 5-ethylidene-2-norbornene copolymer]

<B 'component>
B'-1: Mitsubishi Rayon Co., Ltd. Metablen S-2001 [Silicon core / shell type rubber]
B'-2: G-1651ES manufactured by Kraton Polymer Co., Ltd. [styrene / butadiene / styrene / ethylene copolymer]
<C component>
C-1: EP2601 [Epoxy group-containing silicon elastomer] manufactured by Toray Dow Corning Co., Ltd.
<C 'component>
C'-1: Toray Dow Corning Co., Ltd. EP5500 [silicone elastomer containing no epoxy group]
C'-2: Bond First 7M [Epoxy group-containing ethylene / methyl methacrylate copolymer] manufactured by Sumitomo Chemical Co., Ltd.

<D component>
D-1: Irganox 1076 manufactured by BASF Japan Ltd. [n-octadecyl-3- (3 ′, 5′-di-tert-butyl-4′-hydroxyphenyl) propionate]
D-2: Songwon International Japan Co., Ltd. SONGNOX6260PW [Bis (2,4-di-tert-butylphenyl) pentaerythritol diphosphite]
D-3: Sandstub P-EPQ [tetrakis (2,4-di-tert-butylphenyl) [1,1-biphenyl] -4,4′-diylbisphosphonite] manufactured by Clariant Japan Co., Ltd.
D-4: Adeka Corporation Adeka Stub AO-412S [3-laurylthiopropionate]

Examples 1-12, Comparative Examples 1-12
(Adjustment of composition)
Using PEN-1 as component A, the compositions shown in Tables 2 and 3 were uniformly premixed by dry blending, and then the premixed mixture was supplied from the first supply port of the melt extruder and melt extruded to be pelletized. did. Here, the first supply port is a base supply port. The melt extrusion was carried out using a vent type twin screw extruder (TEX30α-38.5BW-3V manufactured by Nippon Steel Works, Ltd.) having a diameter of 30 mmφ equipped with a side screw. The extrusion temperature is C1 / C2 / C3 to D = 80 ° C./200° C./300° C., the main screw speed is 150 rpm, the side screw speed is 50 rpm, the discharge rate is 20 kg / h, and the vent pressure reduction is 3 kPa. It was.

(Blow molding)
The obtained pellets were dried with a hot air dryer at 160 ° C. for 5 hours, and then a preform was formed. The molding machine used EC160NII-4Y manufactured by Toshiba Machine Co., Ltd. was molded at a cylinder temperature of 290 ° C., a mold temperature of 20 ° C., and a cooling time of 20 seconds to obtain a preform having a thickness of 4.2 mm. A side view of the obtained preform is shown in FIG. In FIG. 1, A-1 is the mouth of the preform, A-2 is the neck of the preform, A-3 is the shoulder of the preform, A-4 is the body of the preform, and A-5 is the preform. At the bottom. Next, using the FDB-1D manufactured by Frontier Co., Ltd. as a blower, using a 1.5 L container-shaped blow mold (vertical 2.3 times × horizontal 3.4 times), the preform as described below. The biaxial stretch blow molding was performed. The preform preliminarily heated in a hot air dryer at 100 ° C. for 1 hour was set in a blow molding machine, the output of the IR heater was set so that the preform surface temperature was 150 ° C., and the main heating was performed. Subsequently, rod stretching speed 60%, primary blow delay time 0.2 seconds, primary blow time 0.3 seconds, primary blow pressure 1.2 MPa, secondary blow time 1.2 seconds, secondary blow pressure 3 Molding was performed under conditions of 0.4 MPa and a mold temperature of 20 ° C., and blow molding was performed. A side view of the obtained blow molded article is shown in FIG. In FIG. 2, B-1 is the mouth of the blow molded body, B-2 is the neck of the blow molded body, B-3 is the shoulder of the blow molded body, B-4 is the body of the blow molded body, and B- Reference numeral 5 denotes the bottom of the blow molded article. Each evaluation of said 2 (1) (i)-(vi) was performed about the obtained blow molded object. The results are shown in Table 2 and Table 3. Tables 2 and 3 also show the results of the physical property evaluations 2 (2) (i) to (iv) described above for the pellets of each example.

Example 13
Except that PEN-2 produced in Production Example 1 was used as the A component, pelletization was performed in the same manner as in Example 1, and physical properties of the above 2 (2) (i) to (iv) were evaluated. Furthermore, blow molding was performed by the same method as Example 1 using the obtained pellet, and each evaluation of said 2 (1) (i)-(vi) was implemented about the obtained blow molded object. The results are shown in Table 2.

Example 14
Except that PEN-3 produced in Production Example 2 was used as the A component, pelletization was performed in the same manner as in Example 1, and physical properties of the above 2 (2) (i) to (iv) were evaluated. Furthermore, blow molding was performed by the same method as Example 1 using the obtained pellet, and each evaluation of said 2 (1) (i)-(vi) was implemented about the obtained blow molded object. The results are shown in Table 2.

Example 15
Except that PEN-4 produced in Production Example 3 was used as the A component, pelletization was performed in the same manner as in Example 1, and physical properties of the above 2 (2) (i) to (iv) were evaluated. Furthermore, blow molding was performed by the same method as Example 1 using the obtained pellet, and each evaluation of said 2 (1) (i)-(vi) was implemented about the obtained blow molded object. The results are shown in Table 2.

Example 16
Pelletization was performed in the same manner as in Example 1 except that PET-1 was used as the component A, and physical properties of the above 2 (2) (i) to (iv) were evaluated. Blow molding was performed by the following method. The obtained pellets were dried with a hot air dryer at 160 ° C. for 5 hours, and then a preform was formed. The molding machine used EC160NII-4Y manufactured by Toshiba Machine Co., Ltd. was molded at a cylinder temperature of 290 ° C., a mold temperature of 20 ° C., and a cooling time of 20 seconds to obtain a preform having a thickness of 4.2 mm. Next, using the FDB-1D manufactured by Frontier Co., Ltd. as a blower, using a 1.5 L container-shaped blow mold (vertical 2.3 times × horizontal 3.4 times), the preform as described below. The biaxial stretch blow molding was performed. The preform preliminarily heated in a hot air dryer at 60 ° C. for 1 hour was set in a blow molding machine, the output of the IR heater was set so that the preform surface temperature was 100 ° C., and the main heating was performed. Subsequently, rod stretching speed 60%, primary blow delay time 0.2 seconds, primary blow time 0.3 seconds, primary blow pressure 1.2 MPa, secondary blow time 1.2 seconds, secondary blow pressure 3 Molding was performed under conditions of 0.4 MPa and a mold temperature of 20 ° C., and blow molding was performed. Obtained with the blow molded article were each evaluated in the 2 (1) (i) ~ (vi). The results are shown in Table 2.

The following can be said from the results shown in Tables 2 and 3 above.
The resin compositions of Examples 1 to 16 were free from axial displacement and breakage of stretch blow molded products, were excellent in appearance, and were excellent in notched Charpy impact strength at 23 ° C. and −60 ° C. Moreover, the further improvement of impact resistance was seen by adding heat processing to an ISO test piece.
On the other hand, in the case of the comparative example 1 which used PEN-1 as it was, it was a result inferior to the Charpy impact strength with a notch of 23 degreeC and -60 degreeC.
In the case of Comparative Example 2 containing only the A component and the B component, the pearl-like appearance was seen in the blow molded product, and the result was inferior to the notched Charpy impact strength at -60 ° C.
In the case of the comparative example 3 which does not contain D component, it was a result inferior to -60 degreeC notched Charpy impact strength.
Furthermore, in the case of the comparative example 4 which used C'-1 component without using C component, the pearl-like appearance was seen by the blow molded product, and it was a result inferior to -60 degreeC notched Charpy impact strength.
In the case of Comparative Example 5 using the C′-2 component without using the C component, the result was inferior to the notched Charpy impact strength at −60 ° C.
In the case of Comparative Examples 6 and 7 using the B′-1 component or the B′-2 component without using the B component, the results were inferior to the notched Charpy impact strength at −60 ° C.

Comparative Example 8 was inferior in notched Charpy impact strength at 23 ° C. and −60 ° C. because the content of the B component was too small.
In Comparative Example 9, since the content of the B component was too large, the appearance of the blow molded product was broken and the wall thickness of the container body was thin.
In Comparative Example 10, since the content of the C component was too small, the appearance of the blow-molded product was pearly and the result was inferior to the -60 ° C notched Charpy impact strength.
Since the comparative example 11 had too much content of C component, surface roughness was seen in the external appearance of the blow molded product.
Finally, Comparative Example 12 had a result that the yellowness of the blow molded product was strong and inferior in hue because the D component content was too large.

Claims (4)

(A) 100 parts by weight of an aromatic polyester resin, (B) 5 to 80 parts by weight of an ethylene / α-olefin copolymer, (C) 1 to 30 parts by weight of an epoxy group-containing silicon elastomer, and (D) a hindered phenol compound, A resin composition comprising 0.01 to 3 parts by weight of at least one antioxidant selected from the group consisting of phosphite compounds, phosphonite compounds and thioether compounds. The resin composition according to claim 1, wherein the ethylene / α-olefin copolymer is an ethylene / α-olefin copolymer modified with an unsaturated carboxylic acid or an acid derivative thereof. The aromatic polyester resin comprises at least one selected from the group consisting of a dicarboxylic acid component dicarboxylic acid of 80 to 100 mol% naphthalene dicarboxylic acid and 0 to 20 mol% terephthalic acid and isophthalic acid, the resin composition according to claim 1 or 2 diol ing ethylene glycol. The molded article of the resin composition according to any one of claims 1 to 3 , wherein the glass transition temperature of the aromatic polyester resin is -40 ° C, and the glass transition temperature of the aromatic polyester resin is 40 ° C. A method for improving low-temperature impact resistance of a molded product, characterized by heat-treating in a temperature range.